EP0700253A1 - Cheesemaking with recombinant aspartic protease - Google Patents
Cheesemaking with recombinant aspartic proteaseInfo
- Publication number
- EP0700253A1 EP0700253A1 EP94913508A EP94913508A EP0700253A1 EP 0700253 A1 EP0700253 A1 EP 0700253A1 EP 94913508 A EP94913508 A EP 94913508A EP 94913508 A EP94913508 A EP 94913508A EP 0700253 A1 EP0700253 A1 EP 0700253A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- milk
- process according
- aspartic protease
- protease
- recombinant
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C19/00—Cheese; Cheese preparations; Making thereof
- A23C19/02—Making cheese curd
- A23C19/032—Making cheese curd characterised by the use of specific microorganisms, or enzymes of microbial origin
- A23C19/0326—Rennet produced by fermentation, e.g. microbial rennet; Rennet produced by genetic engineering
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/48—Hydrolases (3) acting on peptide bonds (3.4)
- C12N9/50—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
- C12N9/58—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from fungi
Definitions
- This invention relates to a process for producing cheese in improved yields.
- the glycosylation of the aspartic protease can give an increase in cheese yield of 0.2% compared with the native enzyme.
- An increase in cheese yield of 0.2% would mean an extra 2 kg of cheese per one ton of cheese having a value of about 8 - 10 US$ (prices of the dairy) .
- the present invention relates to a process of producing cheese in improved yields, wherein a recombinant aspartic protease is added to milk in sufficient amounts to effect clotting of the milk, after which the resulting curd is processed in a manner known per se for making cheese.
- the term "recombinant aspartic protease” is applied to (pro)chymosin or microbial aspartic protease produced in a host organism transformed with DNA coding for the protease.
- the host organism may conveniently be a fungus, e.g. a yeast or a fi1amentous fungus.
- filamentous fungus is intended to include fungi belonging to the groups Phycomycetes, Zygomycetes, Ascomycetes, Basidiomycetes or fungi imperfecti, including
- Hyphomycetes such as the genera Asperqillus r Trichoderma.
- Penicillium f Fusarium or Humicola Penicillium f Fusarium or Humicola.
- recombinant aspartic protease from Mucorales e.g. Rhizomucor r in particular Rhizomucor miehei or Rhizomucor pusillus
- Asperqillus or Trichoderma a process of producing cheese in improved yields.
- a DNA sequence encoding bovine prochymosin or preprochymosin may for instance be obtained as described in EP 215 594.
- a DNA sequence encoding Rhizomucor miehei aspartic protease may be isolated as described in EP 238 023.
- DNA sequences encoding functions facilitating gene expression typically comprise a promoter, transcription initiation sites, and transcription termination and poly- adenylation functions.
- the promoter which may be preceded by upstream activating sequences and enhancer sequences as known in the art may be any DNA sequence exhibiting a strong transcriptional activity in filamentous fungi and may be derived from a gene encoding an extracellular or intracellular protein such as an amylase, a glucoamylase, a protease, a lipase or a cellulase.
- suitable promoters are those derived from the gene encoding h__ oryzae TAKA amylase, Rhizomucor miehei aspartic proteinase, A. niqer neutral ⁇ -amylase, A. niqer acid stable ⁇ -amylase, A. niqer glucoamylase, Rhizomucor miehei lipase, A. oryzae alkaline protease or A. oryzae triose phosphate iso erase.
- the filamentous fungus host organism may conveniently be one which has previously been used as a host for producing recombinant proteins, e.g. a strain of Asper illus sp. , such as A. niqer. A. nidulans or A. oryzae. The use of A. oryzae in the production of recombinant proteins is extensively described in e.g. EP 238 023.
- Termination and polyadenylation sequences may suitably be derived from the same sources as the promoter.
- the techniques used to transform a fungal host cell may suitably be adapted from the methods of transforming A. nidulans described in, for instance, Yelton et al., Proc. Natl. Acad. Sci. USA 8_1, 1984, pp. 1470-1474, or EP 215 594, or from the methods of transforming A. niqer described in, for instance Buxton et al.. Gene 37. 1985, pp. 207-215 or US 4,885,249, or from the method of transforming A. oryzae described in EP 238 023.
- the host cell is transformed with a vector system comprising a DNA sequence coding for a selection marker which is capable of being incorporated in the genome of the host organism on transfor- mation, but which is either not expressed by the host before transformation or expressed in amounts which are not sufficient to permit growth under selective conditions.
- Transformants can then be selected and isolated from non-transformants on the basis of the incorporated selection marker.
- Suitable selection markers are derived from the A. nidulans or A niqer arqB gene, the A. nidulans trpC gene, the A. nidulans amdS gene, the Neurospora crassa pyr4 or DHFR genes, or the A. niqer or A. oryzae niaD gene.
- the DNA sequences coding for the aspartic protease, promoter and terminator may be inserted in a vector containing the selection marker, or it may be inserted in a separate vector for introduction into the host cell.
- the term "vector system" is intended to include a single vector or two or more vectors which together contain the total DNA information to be introduced into the host cell.
- the vector or vectors may be linear or closed circular molecules.
- the vector system comprises two vectors, one carrying the DNA sequence coding for the selection marker, and the other carrying the DNA sequences encoding the he e protein, the preregion and the functions facilitating gene expression.
- the extent of glycosylation of the recombinant aspartic protease has surprisingly been found to be higher than the glycosylation of the aspartic proteases obtained from naturally occurring Rhizomucor strains. More specifically , the novel recombinant aspartic protease is characterized in that the carbohydrate content is of at least 50% more than the native aspartic protease, preferably the carbohydrate content is of a level of 100% more than the native aspartic protease.
- native aspartic protease is intended to indicate the protease produced by an organism in nature (e.g. in calf stomach or by a microorganism such as Rhizomucor) .
- the amount of N-bound glycosylation is determined as the difference in molecular weights between the aspartic protease and a deglycosylated aspartic protease.
- the deglycosy- lation is performed by Endoglycosidase H (from Genzyme) (removes N-bound glycosylation) using 1 mg/ml protease and a reaction time of 18 hour at 37°C, the Endo H is dosed so that no additional deglycosylation is obtained at increased Endo H dosages.
- the MW weight is measured by SDS-PAGE.
- the amount of N-bound glycosylation is expressed in kD glycosylation per mole protein.
- milk in particular milk from ruminants such as cows, sheep, goats or camels, may be used as the starting material in the process of the invention, e.g. as reconstituted milk, whole milk, concentrated whole milk or skimmilk.
- the milk may be concentrated in various ways such as by evaporation or spray-drying, but is preferably concentrated by membrane filtration, i.e. ultrafiltration in which molecules with a molecular weight of up to 20,000 are allowed to pass the membrane, optionally with diafiltration before or after ultrafiltration, or possibly hyperfiltration in which molecules of a molecular weight of up to 500 are allowed to pass the membrane.
- membrane filtration i.e. ultrafiltration in which molecules with a molecular weight of up to 20,000 are allowed to pass the membrane
- diafiltration before or after ultrafiltration or possibly hyperfiltration in which molecules of a molecular weight of up to 500 are allowed to pass the membrane.
- a starter culture may be added to the milk before or simultaneously with the addition of the recombinant aspartic acid in the present invention.
- the starter culture is a culture of lactic acid bacteria used, in conventional cheesemaking, to ferment the lactose present in the milk and to cause further decomposition of the clotted casein into smaller peptides and free amino acids as a result of their production of proteases and peptidases.
- the starter culture may be added in amounts which are conventional for the present purpose, i.e. typically amounts of about 1 x 10 4 - 1 x 10 5 bacteria/g of cheese milk, and may be added in the form of freeze-dried, frozen or liquid cultures.
- the subsequent steps in the cheesemaking process i.e. further salting, pressing, and ripening the curd, may be conducted in the traditional way of producing cheese, e.g. as described by R. Scott, Cheesemaking in Practise, 2nd Ed. , Elsevier, London, 1986.
- the present invention relates to an aspartic protease preparation in liquid, stabilized, spray-dried, vacuum-dried, freeze-dried or granulated form, or immobilized on a suitable carrier.
- the various ways in which the enzyme preparation may be formulated are well known in the enzyme art, cf. for instance K. Aunstrup et al., "Production of Microbial Enzymes", in Microbial Technology (H.J. Peppier and D. Perlman, Eds.), 2nd Ed., Vol I, Academic Press 1979, pp 295-297.
- the amount of recombinant aspartic protease will vary according to the degree of concentration of the milk, but the enzyme will usually be added in an amount of 1 - 10 KRU per 1 1 of whole milk.
- the rennet strength is determined by using a modified Berridge method (N.J. Berridge, Analyst. 77. 1952, p. 57) where the rennet strength is determined by using a Rennilase ® (Rhizomucor miehei aspartic protease available from Novo Nordisk A/S) powder standard as a reference.
- Rennilase ® Rhizomucor miehei aspartic protease available from Novo Nordisk A/S
- the principle of the method is that the enzyme acts upon a solution of skimmed milk powder containing calcium chloride under standard conditions.
- the time needed from the addition of the enzyme until the reaction mixture begins to show flocculation is measured. This time is approximately inversely proportional with the enzyme concentration and is compared with the flocculation time for a sample with known enzyme strength. These times should not differ substantially from each other, and they should amount to 5.0 min ⁇ 0.5 min.
- the determination of strength is carried out visually and is performed at 30°C.
- "Berridge Substrate" consisting of 12 g of spray-dried skimmed milk powder dissolved in 100 ml of 0.01 M calcium chloride solution is used. The substrate must stand for at least 1 hour before it can be used.
- the analysis is performed in a glass water bath in which the test tubes by means of a motor are slowly rotated about their longitudinal axes with an inclination of about 30° relative to the water surface.
- a film of milk will thereby continuously be formed on the tube above the milk surface, and it is easy to see the flocculation in this film as soon as it starts.
- the enzyme solution is injected against the wall of the tube to avoid foaming of the milk.
- the test tube is closed with a clean, dry stopper and inverted 3 times so as to wash all the enzyme off the tube wall and into the milk.
- the first test tube may immediately thereafter be placed on the rotating spindle.
- the stop watch for the first tube is stopped, the tube is replaced with tube No. 2 etc. Try to achieve a flocculation time between 4.5 and 5.5 min.
- the flocculation time for the 3 test tubes must not vary more than 0.1 min (6 sec), and the average is used to cal- culate the strength of the rennet. Calculation of the Rennet Strength
- the modified Berridge method is only suited for the determination of rennet strengths of rennets without added calcium salts.
- Aspergillus oryzae produced protease Transformant p777 (described in EP 489718) was fermented for approx. 5 days in a conventional agitated and aerated 2.5 m 3 fermentor on a medium containing soya grits supplied with maltodextrin during growth, the pH was kept below 6.0 by addition of phosphoric acid.
- the aspartic protease was recovered from the fermentation broth by conventional filtration, ultrafiltration, and evapora- tion techniques. The aspartic protease was destabilized as described in US Patent 4,357,357.
- the aspartic protease concentrate was diluted to 54.63 KRU/g.
- a starter culture CHL 113 batch 010691 (available from Chr. Hansen, .B ⁇ ge Alle 10, DK-2970 H ⁇ rsholm, Denmark) was incubated for 16 hours in sufficient amount of milk at room temperature and frozen in 40 g portions, enough portions for the entire experiment.
- N was determined using a modified Kjeldal method on a Tecator Digestor and Kjeltec 1003 Distilling System. Protein was expressed as N x 6.38. All analysis were done in triplicate.
- Aspartic protease is a glycosylated protein both when expressed from R. miehei and from A. oryzae.
- Endoglycosidase H can liberate the glyco part from N-glycosylated proteins by specific hydrolysis between two N-acetylglucosamine molecules which are bound to Asn in N-glycosylated proteins.
- the Aspergillus orvzae produced aspartic protease (produced as described in Example 1) was purified from the culture broth by the method described in Journal of Chromato- graphy 476 (1989) 227-233.
- Rhizomucor miehei produced aspartic protease was purified from Rennilase 150 ® L (available from Novo Nordisk A/S) by the method described in Journal of Chromatography 476: (1989) 227-233.
- the MW of the deglycosylated aspartic protease was 38.3 kD both from R. miehei and A. oryzae. whereas the glycosy- lated enzyme from R. miehei showed a MW of 41.5 kD, and the glycosylated enzyme from A. oryzae showed a MW of 44.7 kD.
- N-bound glycosylation content of the A. oryzae expressed aspartic protease is then 6.4 kD (44.7 kD minus 38.3 kd) per mole protein, being 100% more than the 3.2 kD (41.5 kD - 38.3 kD) N-bound glycosylation per mole Rennilase (R. miehei expressed aspartic protease) .
- Example 1 (produced as described in Example 1) was purified from the culture broth by the method described in Journal of Chromato- graphy 476 (1989) 227-233.
- Rhizomucor miehei produced aspartic protease was purified from Rennilase 150 ® L (available from Novo Nordisk A/S) by the method described in Journal of Chromatography 476: (1989) 227-233.
- the monosaccharides were separated and detected by a
- Rhizomucor miehei Aspergillus oryzae produced produced aspartic protease aspartic protease
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Zoology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Molecular Biology (AREA)
- Organic Chemistry (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Wood Science & Technology (AREA)
- Mycology (AREA)
- Biomedical Technology (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Food Science & Technology (AREA)
- Dairy Products (AREA)
- Enzymes And Modification Thereof (AREA)
Abstract
Description
Claims
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK474/93 | 1993-04-27 | ||
DK47493 | 1993-04-27 | ||
DK93474A DK47493D0 (en) | 1993-04-27 | 1993-04-27 | METHOD OF PRODUCING CHEESE |
PCT/DK1994/000163 WO1994024880A1 (en) | 1993-04-27 | 1994-04-22 | Cheesemaking with recombinant aspartic protease |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0700253A1 true EP0700253A1 (en) | 1996-03-13 |
EP0700253B1 EP0700253B1 (en) | 2000-01-05 |
EP0700253B2 EP0700253B2 (en) | 2003-05-14 |
Family
ID=8093958
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP94913508A Expired - Lifetime EP0700253B2 (en) | 1993-04-27 | 1994-04-22 | Cheesemaking with recombinant aspartic protease |
Country Status (11)
Country | Link |
---|---|
US (1) | US5800849A (en) |
EP (1) | EP0700253B2 (en) |
CN (1) | CN1056036C (en) |
AT (1) | ATE188347T1 (en) |
AU (1) | AU677652B2 (en) |
DE (1) | DE69422514T3 (en) |
DK (2) | DK47493D0 (en) |
ES (1) | ES2143545T5 (en) |
GR (1) | GR3032856T3 (en) |
PT (1) | PT700253E (en) |
WO (1) | WO1994024880A1 (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003100048A1 (en) | 2002-05-29 | 2003-12-04 | Dsm Ip Assets B.V. | Method for the purification of microbial protease |
WO2010102976A1 (en) | 2009-03-10 | 2010-09-16 | Dsm Ip Assets B.V. | Pregastric esterase and derivatives thereof |
US7955829B2 (en) | 2001-12-19 | 2011-06-07 | Dsm Ip Assets B.V. | Method for the inactivation of amylase in the presence of protease |
EP2333056A1 (en) | 2006-04-13 | 2011-06-15 | DSM IP Assets B.V. | Liquid composition comprising an aspartic protease |
WO2016135133A1 (en) | 2015-02-27 | 2016-09-01 | Basf Se | A vehicle comprising a storage system and a combustion engine, the storage system comprising a container and at least one storage vessel |
EP3093549A1 (en) | 2015-05-11 | 2016-11-16 | Basf Se | Vehicle comprising an internal combustion engine, at least one storage vessel and a cooling chamber and/or an air condition unit |
EP3130835A1 (en) | 2015-08-13 | 2017-02-15 | Basf Se | A vehicle comprising a storage system and a combustion engine, the storage system comprising a container and at least one storage vessel surrounded by a housing |
EP3130834A1 (en) | 2015-08-13 | 2017-02-15 | Basf Se | A vehicle comprising a storage system and a combustion engine, the storage system comprising a container and at least two storage vessels |
WO2018228966A1 (en) | 2017-06-15 | 2018-12-20 | Dsm Ip Assets B.V. | Frozen enzyme pellets |
EP3653800A1 (en) | 2018-11-15 | 2020-05-20 | Basf Se | Generation of drinking water from air by means of a box, comprising at least one sorption material |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5674728A (en) * | 1993-11-03 | 1997-10-07 | Novartis Corporation | Aspergillus niger vacuolar aspartyl protease |
DE69535877D1 (en) * | 1994-12-21 | 2008-12-11 | Hansens Lab | MICROBIAL PRODUCED RENNIN WITH IMPROVED MILK CREATION ACTIVITY AND METHOD FOR THE PRODUCTION THEREOF |
US6416796B1 (en) * | 1999-04-27 | 2002-07-09 | Kraft Foods, Inc. | Whey protein digestion products in cheese |
AU2003232180A1 (en) * | 2002-06-17 | 2003-12-31 | Chr. Hansen A/S | Improved method of producing an aspartic protease in a recombinant host organism |
WO2005004641A1 (en) * | 2003-07-01 | 2005-01-20 | Novozymes A/S | Compositions and methods for tenderizing meat |
WO2011076123A1 (en) | 2009-12-22 | 2011-06-30 | Novozymes A/S | Compositions comprising boosting polypeptide and starch degrading enzyme and uses thereof |
ES2565060T3 (en) | 2010-04-14 | 2016-03-31 | Novozymes A/S | Polypeptides having glucoamylase activity and polynucleotides encoding them |
WO2017089613A1 (en) * | 2015-11-26 | 2017-06-01 | Csk Food Enrichment B.V. | Liquid composition comprising an aspartic protease having improved enzyme stability |
CN105420220B (en) * | 2016-01-26 | 2018-10-09 | 华东理工大学 | A kind of aspartic acid albuminoid enzyme and its encoding gene and application |
WO2017177153A1 (en) | 2016-04-07 | 2017-10-12 | Novozymes A/S | Methods for selecting enzymes having protease activity |
Family Cites Families (9)
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US3212905A (en) * | 1961-07-20 | 1965-10-19 | Meito Sangyo Kk | Process for making cheese |
US3151039A (en) * | 1961-07-20 | 1964-09-29 | Meito Sangyo Kk | Milk coagulating enzyme "microbial rennet" and method of preparation thereof |
US3295991A (en) * | 1963-02-18 | 1967-01-03 | Evans Res & Dev Corp | Enzymatic process of making cheese and cheese products |
PL193146A1 (en) * | 1976-10-19 | 1978-04-24 | Inst Przemyslu Mleczarskiego | ENZYMATIC PREPARATION FOR RIPENING OF WHITE DAIRY PRODUCTS |
US4885249A (en) * | 1984-12-05 | 1989-12-05 | Allelix, Inc. | Aspergillus niger transformation system |
DK122686D0 (en) * | 1986-03-17 | 1986-03-17 | Novo Industri As | PREPARATION OF PROTEINS |
EP0305216B1 (en) * | 1987-08-28 | 1995-08-02 | Novo Nordisk A/S | Recombinant Humicola lipase and process for the production of recombinant humicola lipases |
DE3729800A1 (en) * | 1987-09-05 | 1989-03-16 | Krups Stiftung | ELECTRICALLY OPERATED STEAM IRON |
DK63490D0 (en) * | 1990-03-09 | 1990-03-09 | Novo Nordisk As | METHOD OF PRODUCING CHEESE |
-
1993
- 1993-04-27 DK DK93474A patent/DK47493D0/en unknown
-
1994
- 1994-04-22 ES ES94913508T patent/ES2143545T5/en not_active Expired - Lifetime
- 1994-04-22 CN CN94191915A patent/CN1056036C/en not_active Expired - Lifetime
- 1994-04-22 WO PCT/DK1994/000163 patent/WO1994024880A1/en active IP Right Grant
- 1994-04-22 DE DE69422514T patent/DE69422514T3/en not_active Expired - Lifetime
- 1994-04-22 AT AT94913508T patent/ATE188347T1/en active
- 1994-04-22 US US08/535,237 patent/US5800849A/en not_active Expired - Lifetime
- 1994-04-22 AU AU65639/94A patent/AU677652B2/en not_active Expired
- 1994-04-22 PT PT94913508T patent/PT700253E/en unknown
- 1994-04-22 EP EP94913508A patent/EP0700253B2/en not_active Expired - Lifetime
- 1994-04-22 DK DK94913508T patent/DK700253T4/en active
-
2000
- 2000-03-03 GR GR20000400548T patent/GR3032856T3/en unknown
Non-Patent Citations (1)
Title |
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See references of WO9424880A1 * |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7955829B2 (en) | 2001-12-19 | 2011-06-07 | Dsm Ip Assets B.V. | Method for the inactivation of amylase in the presence of protease |
WO2003100048A1 (en) | 2002-05-29 | 2003-12-04 | Dsm Ip Assets B.V. | Method for the purification of microbial protease |
US7670821B2 (en) | 2002-05-29 | 2010-03-02 | Dsm Ip Assets B.V. | Method for the purification of microbial protease |
EP2333056A1 (en) | 2006-04-13 | 2011-06-15 | DSM IP Assets B.V. | Liquid composition comprising an aspartic protease |
WO2010102976A1 (en) | 2009-03-10 | 2010-09-16 | Dsm Ip Assets B.V. | Pregastric esterase and derivatives thereof |
WO2016135133A1 (en) | 2015-02-27 | 2016-09-01 | Basf Se | A vehicle comprising a storage system and a combustion engine, the storage system comprising a container and at least one storage vessel |
EP3093549A1 (en) | 2015-05-11 | 2016-11-16 | Basf Se | Vehicle comprising an internal combustion engine, at least one storage vessel and a cooling chamber and/or an air condition unit |
WO2016180807A1 (en) | 2015-05-11 | 2016-11-17 | Basf Se | Vehicle comprising an internal combustion engine, at least one storage vessel and a cooling chamber and optionally an air condition unit |
EP3130835A1 (en) | 2015-08-13 | 2017-02-15 | Basf Se | A vehicle comprising a storage system and a combustion engine, the storage system comprising a container and at least one storage vessel surrounded by a housing |
EP3130834A1 (en) | 2015-08-13 | 2017-02-15 | Basf Se | A vehicle comprising a storage system and a combustion engine, the storage system comprising a container and at least two storage vessels |
WO2018228966A1 (en) | 2017-06-15 | 2018-12-20 | Dsm Ip Assets B.V. | Frozen enzyme pellets |
EP4339279A2 (en) | 2017-06-15 | 2024-03-20 | DSM IP Assets B.V. | Frozen enzyme pellets |
EP3653800A1 (en) | 2018-11-15 | 2020-05-20 | Basf Se | Generation of drinking water from air by means of a box, comprising at least one sorption material |
WO2020099561A1 (en) | 2018-11-15 | 2020-05-22 | Basf Se | Generation of drinking water from air by means of a box, comprising at least one sorption material |
Also Published As
Publication number | Publication date |
---|---|
ES2143545T5 (en) | 2004-02-16 |
DK47493D0 (en) | 1993-04-27 |
DE69422514T3 (en) | 2003-12-24 |
PT700253E (en) | 2000-04-28 |
DK0700253T3 (en) | 2000-04-25 |
DE69422514T2 (en) | 2000-07-06 |
CN1121686A (en) | 1996-05-01 |
DE69422514D1 (en) | 2000-02-10 |
DK700253T4 (en) | 2003-09-01 |
US5800849A (en) | 1998-09-01 |
ATE188347T1 (en) | 2000-01-15 |
GR3032856T3 (en) | 2000-07-31 |
AU677652B2 (en) | 1997-05-01 |
WO1994024880A1 (en) | 1994-11-10 |
AU6563994A (en) | 1994-11-21 |
EP0700253B1 (en) | 2000-01-05 |
EP0700253B2 (en) | 2003-05-14 |
CN1056036C (en) | 2000-09-06 |
ES2143545T3 (en) | 2000-05-16 |
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